Phenol recovery



E. L, POLLITZER PHENQL RECOVERY Filed oofc.' "16,

' /fF'racf/onat/nn Zone A A.25A

\ N Hydroganaf/'Qn Zone Y Frqcf/"nnaf/ bn Zone OQ Condense( Dehydaf/'on VZone /N VEN TOR: Eines! L. Poll/'tzer @mja A TTOP/VEYS e i 4. 3,205,272` i PHENOL RECOVERY' Ernest Pollitzer, Hinsdale,- lll., Vassigner-"to Universal' Uil AProducts Company,- Des Plaines, IlL, a corporation of Delaware Filed Oct. 16,1961,v Ser. N0. 145,227 l 6 Claims. '(Cl. 2604-621) Patented Sept. 7, 1965 embodiesy an improvement which comprises passing said reaction mixture toa separati on zone and therein distilling the acetone fraction fromsaid reaction mixture, passing the' acetone-free reaction mixture to a dehydration zone which isin open-communication with a fractionation zone, .dehydrating the alpha,alpha-dimethylbenzyl alcohol portion of said reactionmixture to form additional alphal V This invention relatesto there'covery o'f'a phenol from y a reaction'` mixture .resulting from"thedecompositiori of ,an aralkyl tertiary hydroperoxide, and in particular to the ,recovery `of phenol from a reactionmixture' resulting from the decomposition ofcumene hydroperoxide.

. lPhenols are readilyprepared by the oxidation of an `aryl i tertiary alkane and the subsequent decomposition of the Vresulting aralkyl tertiary hydroperoxide to form a' decomposition reactionumixture'comprising a phenol,` a ketone, and unreactedaryltertiary'alkane. For example, phenol 'is prepared by theoxidation of cumene and the subsequent decomposition of the resulting cumene hydroperoxide to form a reaction mixture comprising phenol, acetone, and unreacted cumene.. In'addition to the phenol, ketone, and

aryl. tertiary valkane, the .decomposition'reaction mixture methyh styrene by contacting said reaction mixture wit-l1 iodine in the aforesaid dehydration zone -at a temperature of, from aboutl 80 C. to about ll0 C. and at a reduced v prcssureof from 3.2 Hg to about 9.4 Hg, separating the resulting reaction mixture into a phenol fraction, an alpha-methyl styrene-phenol fraction, and a cumene fraction at substantiallythe aforesaid conditions of reduced pressure in saidope'nly communicating fractionation zone, separately recovering the curnene fraction and the phenol fraction, conducting the methyl styrene-phenol fraction to :la hydrogenation zone and converting the methyl styrene to n cuiuene therein by contacting said methyl styrene-phenol ffraction'with hydrogen in the presence o f a catalyst corn- .prisirig nickel on a silica-alumina support andata temperature of from about 20 -C. to about-75" C. and at a.

' pressureoi from about 25 p.s.i.g. to. about 125 psig.,

further comprises small -amounts of fan aryl tertiary alkene I andanl aryl tertiary alkanol derivative of the laryl tertiary, alk'ane subjected `to oxidation in the rst instance. In theY case o f curnene hydroperoxide, derived from the oxidation -of'cune'ne, the aryltertiaryalkene isaIpha-methyIstyrene and -the aryl tertiary alkanol-is alpha, alpha-,dimethyl-V `benzylalcohol. A In the recoveryof phenolfrom the aforesaid reaction mixture bydistillation methods,- the reaction I mixture is exposed toconditions yconduciveto polymeriza-A tion and alkylation'involving the activephenol nucleus,v thel alpha-methylstyrene,- andthe alpha, alpha-dimethylbenzene alcohol. Asa result, the over-all yield'of-the productsv formed` to adversely effect the recovery lof a i 'substantially pure phenol product.'

-desiredphenolproduct sreducedand undesirable by-v ,It is an object ofv the present invention to provide a lnovel process for the recovery of a' phenol from a reaction .mixture resulting from the decomposition of an aralkyl tertiary hydroperoxide.

'.It is a more specific object to present a process for the recovery of phenol from a reaction mixture resulting from `the decompositionY of cumene, hydroperoxide, and' compassing the resulting c umene-phenol solution to a second .fractionation zone, separating and recovering the cumene as the overhead distillate and separately recovering the phenol. l

Further objects and embodiments of the present invention` will become apparent in the following. detailed desc :ription thereof.

In accordance with the process of this invention a phei no1 isrecovered from a reaction mixture resulting from the decomposition of an aralkyl tertiary hydroperoxide.

The -aralkyl tertiary hydroperoxides of this invention are the oxidation products of arylalkanes, and particularly aryl tertiary alkanes. For example, aryl tertiary alkanes including cum'ene, p-cymene, p-isopropylethylbenzene, p-

diisopropylbenzene, p tbutylisopropylbenzene, sec-butyl-` benzene, diphenylethane, 2-isopropylnaphthalene, and the like, maybe oxidized to their corresponding hydroperoxides', i.e., cumene hydroperoxide, alpha, alpha, 4-trimethylprising phenolacetone,alpha, alpha-dimethylbenzyl alcof hol, alpha-methyl styrene, and unreacted cumene, whereby said alcohol and'saidrnethyl styrene are separated from. the reaction mixture prior to exposure to process condi tions conducive Vto undesirable by-product formation.

In one of its broader aspects the present invention relates f to the recovery of a phenol froma reaction mixture resulting from the decomposition of an aralkyl tertiary hydroperoxide and comprising said phenol, a ketone,-an aryl tertiary alkanol and an aryl tertiary alkene, and embodies an improvement in the process of recovering the phenol from saidreaction mixture which comprises distilling the ketone from said reaction mixture, dehydrating th'e aryl tertiary alkanol and forming additional aryl tertiary alkene by contacting the ketonefree reaction mixture with iodine in a dehydration zone at dehydration reaction-conditions comprising an elevated'temperature and a reduced pressure, separating the resulting reaction mixture into a phenol fraction and an aryl'tertiaryV alkene fraction ina fractionation zone, said fractionation zone being in open communication with. the aforesaid dehydration zone, and

' separately recovering said phenol fraction.

` Mores`peciiically, the present invention relates to theV recovery of phenol from a reaction mixture resulting from the decomposition of cum'e'ne hydroperoxide and comprising said phenol, acetone, alpha-methyl'- styrene, alpha,

. alphaalimethylbenzyl alcohol, and unreacted cumene, and

from the group consisting of alkyl, cycloalkyl, aryl, aralkyl` benzyl hydroperoxide, ,Ll-ethyl-alpha, alpha-dimethylben- Avzyl hydroperoxide, alpha,'alpha, alpha', alphatetrameth ylp-xylylene dihydroperoxide, ptbutyl-alpha,alphadi rnethylbenzyl hydroperoxide, alpha-methyl-alpha-ethylbenzyl hydroperoxide, alpha-methyl-alpha-phenylbenzyl hydroperoxide, Z-naphthyl-dimethylmethyl hydroperoxide, etc; The nralkyl tertiary hydroperoxide's, ofwhich the above are illustrative, may be represented by the general formula l wherein Ar represents an aromatic hydrocarbon radical which may be an aryl radical or an alkaryl radical, and the hydroperoxyl group Q-O-H) is attached to a tertiary carbon atom, whichin turn is attached to the aromatic nucleus by a single bond,` and R1 and R2 may be the same or different hydrocarbon radicals selected and alkaryl hydrocarbon radicals.

In the preparation of phenols by the oxidation of an. aryl tertiary alkane and decomposition of the resultingf aralkyl tertiary -hydroperoxide there is formed, in addition to the desired phenol product, an undesirable alcohol and anyolen by-product herein described as an arylalkene and an arylalkanol derivative of said aryl tertiary alkane subjected to oxidation in the rst instance. The unsaturation in the alkyl tertiary olefin, and the hydroxyl group of the aryl tertiary alkanol, occurs at the tertiary carbon atom v 3 attached to the aromatic alkane.' f

Thus the'pr'ocess of the prescnt'inventiorirelatesto the recovery-'of a lphenol from u reaction mixture 'resulting ture resulting from lthe decomposition'of alpha,'alph a,4-

trim'ethylbenzyl hydroperoxide and comprisingp-cresol; acetone, alpha,alpha,4.trimethylbenzyl alc'ohol, "dimethyl styrene, vand vunracted p-cymene, thev recovery of p-ethylphenol from a reaction `mix tu re resulting from'l alphaA- the'A decomposition of lethyl-alpha,v -alpha-dim'ethylbenzyl hydroperoxide and .comprising '1J-ethy1p'he-nol, acetone, 4-ethyl-alpha,alpha-dimethylbenzyl alcohol, 't-cthyl-alphamethyl styrene, 'andunre'acted p-ethylisopropylbenzene,

also vto the recovery tot: phenol from a react'ion mixture` resulting 'from the decomposition of ,alpha-methyl-alphaethylbenzyl hydroperoxide and comprising phenol, `2

vbutanone, aIphmethyl-alpha-ethylben'zyl alcohol, alphaethyl styrene, and unreact'ed seC-butylbenzenef,etc.`

' While the process'of this-invention is voperable tore- 'over a phenolfromfa reactionfmixture.'resulting from y y the decomposition of other aralkyl tertiary hydroperoxides Ias described above, it isprir'narily directed tothe recovery yof phenol from. areaction mixture resulting from the' d eiucomposition of cumene hydroperoxide,' and vthe further 4description lofthe process of this invention isset out in relation. theretol and vwith referenceto the-'attached schematic drawing.

alpha-methyl'. styrene, and unreacted cu1ne`ne, is charged through line 1 .to a distillati-on zone Zoperated at siib-v stantiallyatmospheric pressure, wherein the acetoneA isi .'-distilledfrom the reaction mixture and passes overhead through line` 3 toV storagefac'ilities not shown.'

' .The ,acetone-free decomposition reaction' mixture'i is withdrawn from .the base of said separation zone 2 through,-l i

a conduit 4. and.;pas'ses to :af-pressure 4reducing valve 7 by way vof line k6 in the presence"of-iodine introduced thereto by meansl of an inletS. The reaction mixture nucleusof said aryl tertiary During the course of passage through the dehydration zone 9, the alpha, .alpha-dirncthylbenzylV alcohol is con- Cil' verted to alpha-methyl. styrene. The methyl styrene, phenol, and cumene portion of the resulting reaction mixture distill'supwardly vfrom thedehydration zone through the vaforementioned openly communicatingfractionation zone 10 and is separated therein into-"a phenol fraction withdrawn through a 'takeoff line 1l, a methyl. styrene- 'the overhead distillate.

phenol fraction'withdrawnthrough a second take-off line 12, and a cumene fraction withdrawn through line 13'as Ahigher boiling portion of the aforesaid resulting reactionmixture continues downwardly lthrough the dehydration zone 9 and exits there- ,from lthrough line '36 and is discharged at atmospheric pressure Vby means 'of'a'pumpv 37 and outlet 38. The' higher boil'ingportion, comprising .acetophenone and 'other higher boiling by-products of `;catalyst replacement' are not necessitated. While the dehydration and fractionation step 'above describedl may be rcaction, is separately recovered. v. The aforesaid methodis' particularly adapted to a con- 'tinuousztype of operation in that periodic-shut 1downs for the decomposition accomplished at atmospheric pressure, it'isjpreferred to .operate at the aforesaidconditions of reduced pressure.

I n so doing, the alpha, alpha-dimethylbenzyl alcohol portion of the reaction mixture is convertedto'alpha-methyl styrene at the relatively mildfdehydration reaction conditions herein employed in conjunction with iodine, and said alpha-methyl styrene is' separated substantially immediately as formed. Thus, the reaction mixture is n'ot unduly exposed toA dehydration and fractionation conditions with -risk of undesirable'by-product'formation.

Q Referringl then to the drawingi the 'cumene' hydropcroxide decomposition reactionimixture, resul-ting' from. the decomposition of cumeney hydroperoxide andfcornprisingv acetone,;"phenol,' alpha,- alpha-dimethyl-benzyl alcohol,v

.The'phenol fraction, omprising the major portion of l thejphenol product, is conducted by way-0f `line 11 to a pump 14v and discharged therefrom' to line 15 at substantially'atmospheric pressure. The cumene fraction, withdrawn through line 13 as the overhead-distillate, is condensed in an overhead condenser 31 and withdrawn therefrom through line 32 to a pump 33 and discharged therefrom to line 34 at 'substantially atmospheric pressure.

4The iodine is converted to hydrogen iodidein the dehydration .process and passes upwardly through the frac- Jtionation .zone passing yoverhead throughline 13 and the passes through vsaid pressure" reducing' valve to a dchy-f dration vzone 9 by way of line .The dehydration zone` isinopen communication 'with a fractionationzonev 1{i,` said dehydration zone andsaid `fractionationzone being'.

maintained at a reduced Hpressure offrom. about 0,8" Hg to about-16.5 Hg; and preferably at a pressure of from -about3.2"-Hg'to` about 9.4 Hg( f vThe decomposition reactionmixture desccndsthrough t the dehydration zone 9, whichmay comprise either a column containing an inert packing such as glass beads or. unpaclged column, in the presence'of the. aforementioned iodine at a temperature of from about 50! C. to

about .130 C., and preferably at a temperature of from about 80 `C. to about-,110 C. The alpha-alpha-dimethyl'benzyl alcohol portion of the decomposition reaction mixture4 is dehydrated to-alpha-methyl styrene dur- ;ing passage through the dehydration zone at the aforesaid :dehydration -temperature by the action of catalytic' amounts of iodine which'may comprise from about,0.005 wt.' to about 0.1 wt. of the decomposition reaction imixtu're introduced through line 8. While 'larger quantities ofjiodine are operable', no' particular benet results by reason' thereof and it is preferred to utilize an amount 1 within the aforesaid limits.-

overhead condenser 31 and exits therefrom through line 35. Line '35 is routed to a vacuum source not shown which `may be adequately protected .from the hydrogen iodideby a caustic scrubber,

The cumene stream 'from line 34 is combined with a cumene stream from line 29, said stream being formed as hereinafterdescribed,'and the combined streams pass by way of, line 30 to a caustic scrubber 39. The caustic scrubber, which may comprise sodium bicarbonate, sodium hydroxide, etc.' in aqueous solution or in a granular form, serves to eliminate any residual hydrogen iodide which mayA be' present in the cumene stream as a result of the vdehydration reaction in the dehydration zone 9. The cumene stream thus treated exits through line 40 to be recycled for oxidation to cumene hydroperoxide or otherwise utilized The methyl styrene-phenol fraction, withdrawn from the fractionation zone 10 through the take-ott line 12, is generally withdrawn as an azeotropic mixture cornprising about 95% alpha-methyl styrene. This azeotropicv mixture is discharged to 'line 17 under pressure by means of pump 16 and passes through a heat exchanger 1S wherein it is cooled so as to maintain a desired ternvperature of from about 25 C. to about 75 C. in the hydrogenation zone 22. The cooled methylstyrenephenol stream then passes by way of line 19 to be admixed with a hydrogen stream introduced through an inlet 20, and the combined streams are charged through line Z1 to a hydrogenation zone 22 at a pressure of from about 25 p.s.i.g. to about 125 p.s.i.g.

The methyl styrene-phenol 'fraction isv charged to thev hydrogenation zone 22 and thev methyl styrene portion thereof'converted to cume'ne'. in the presence' of a hydro- I 'claim as my invention: 1; -In a process for therecovery of a phenol from a reaction mixture resulting from the decomposition of an ar'alkyl tetiary hydroperoxide'and comprisin'gsaid` phenol, a ketone, an aryl tertiary alkanol and an 'aryl tertiary Y', alkene, the improvement which comprises distilling the distilled from vthe phenol -and'passes overhead to :line 29 to co'mbine with the cumene l stream from line 3 4. The

combined lstreams exit" from the 'recoveryl process through line 30, the v'aforementioned caustic scrubberf39j `and line -i i 1 40. vThe s'mall'amoniits .of'water which maybecont'ainedg' in the Curnenestream, either a' result ofthe dehydration j reaction or the use of-anaqueous causticscrubbenniay zbe removed by, any conventional for convenient drying methods.-

v,Phenol iswahdrwn fiprfihsdisginlaaa ane 27 and is methods without th eyformation ofv the undesirable. 'alkyl ation and polymerization b y-prod'ucts` resulting from then presence, o falpha, ;y alpha-dirnethylbenzyl'. alcohol and valpharnetliyl styrene. 5

v -A vhydrog'enatio'n ca talyst'iswutilized in the hydrogena- 'tionizone 22 which` is sufficiently active to `selectivelyhyf jdrOgenate -methyl styrene in the'presen'ce of phenolat the relatively mild hydrogenationconditions'herein employed.

"Particularly good results have beenachiev'ed through' the `utilization of, palladium 'on'a silicafalumina support, andy .also nickel 'on' a 4silica-aluininasupport. '.Copper, fishro^ mium, andthemetal'sof Group VIIIincluding iron, co,

f balt, platinum,C osmi'um, iridium',"ruth`enium,rhodiurng and` the aforementionedpalladium and nickel are also .suitable i and may be l'employed either vin al finely vdividedstate or, l

" pifeferably,deposited "on" a svuppo'rting.'materialy such'as andthe like." The oxides of the aforementioned'.metals,

' vandin particulanthe`oxidesf-ot'copper, chromium and nickel, are alsorsuitable' catalysts.

' `The-'foregoingides'criptionof the tion illustrates schematically .one preferred methodyof )perationlA It is understood that many mo' d 'iiicatioi isandl variations'maybe, made `tl'1 eretc without departing from process of-1thisfini/ern.`

ketone `fromsaidgreaction mixture, subjecting the ketonefree mixture tofd'ehydrationto convert the .aryl tertiary .alkanol into additional aryl tertiaryI alkene, separating without' hydrogenatio'n of the phenol by contacting said last'named fraction with hydrogen in the presence of a hy- .drog'en'ation catalyst comprising a' G1',0 UP VIII metal at a temperature `of rornabout 20 C. to about 75 C. and

- yMap-fessure of fromabotitf p.s.i.g. to about 125 p.s.i.g.,

if recovered through line 28 in combinati'onwith thephenol stream from line 15. The .phenol is thus recovered in increased yield :and may .beirther purifiedxby, distillation fractionating". the resultant'products to separate said alkane from the phenoL'ommingling the last-mentioned phenol 'with said phenolgfraction and recovering the resultant mixture.

l2. The improvement of claim 1 further characterized in that said ketonelfr'ee `mixture is subjected to dehydration in the-presence of iodine.

3. In a process for the'recovery 'of phenol from a ref f ac tion-mixture resulting from the decomposition of cum'ene hydroperoxide and comprising said phenol,- acetone, alpha, alpha-dimethyl-benzyl alcohol and alphamethyl styrene, the improvement which comprisesdistilling the acetone 'from said reaction mixture, subjecting the acetonefrcernixture to dehydration to convert the alpha, alpha- `dimethylbenzyl alcohol into Vadditional alpha-methyl` styrene, separating from'the resultingrreactio'n mixture aphenol fraction' and an az'eotropic mixture of phenol and alpha-methyl styrene, subjecting saidazeotropic mix- .tureto selective `hydrogenation to convert the methyl styrene' to cumene 'i/vithout hydrogenation of the phenol by contacting saidi-a'zeotropic mixture with hyrogen in the 4U presence of a hydrogenation catalyst comprising a Group VlIIumetal at a temperature offrom about 20 C. `toabout 75 (land ata pressure of from about 25 p.s.i.g.

to'about 125 p .s.i.fg., fractionatng the resultant products 5to separate the cumene from the phenol, commingling the thelgenerallybroadscope of this invention as set'out in the resulting reactionmixture" is fractionated at reduced pres; s'ure `andthe .umene,'phenol', vand.'acetophenone cuts are separated and recovered.A The alpha-r'nethyl styrene cut j isA recoveredfas an'azeotropic mixture with phenol, the phenol comprising aboutj5% thereof.

A- hydroge'tion catalyst was-prepared byimmersing 150 gms. of Isilicaaluminacracking catalyst in an aqueoussolution'of 2.5 gms of palladium chloride] The catalyst wasdried and calcined at'about 1300? F. Alpha-methyl styrene was processed over; this catalyst .in the presenceof phenol and hydrogenat aboutQ p.s. i.g.'and atl atem'per- 4attire of about 7555C. Infrared analysis indicated substantially complete conversion Qt'IheaIpha-mElhyl ystyrene to cumene, andra phenol fraction substantially unaf- I fected'fby the hydrogenation conditionsemployecl.

last-mentioned phenol with said phenol fraction, and recovering the resultant mixture.

v 4.71`hje improvement vof cl'aimf3 further characterized in that said acetone-free mixture is subjected to dehydrationin the presence of iodine.

f5.1' I nla process Lfor the recovery of phenolffrom a rei action mixture-resulting from the decomposition of cumene hydroperoxide andcomprising said phenol, acetone;

' alpha, falphadimcthylbenzyl alcohol and alpha-methyl styrene, theimprovement whichcomprises distilling the acetone fromsai'cl reaction mixture, dehydrating the alpha,

alpha-dimethylbenzyl alcohol and forming additional yalpha-niieth'yl styrene by contacting the acetonefree reaction mixture with iodine in a dehydration zoneat a temperature of fromabout 50 Cito about 130 C.v and at a lreduced pressureof from `about`:'0.8" Hgto about 16.5"

:1I-Ig, separating from the resulting reaction mixture a phenol fraction and an azeotropic mixture of phenol and alpha- -r methyl styrene, subjecting said azeotropic'rnixture to selective hydro'genation toconvert the methyl styrene `to cumene without hydrogenat'ion of the phenol by contacting `saidazeotropic mixture with hydrogen in the presence of a'hydrogenation catalysticomprising a Group VIII -me`tal at a temperature of from about 20 C. to about C. fand at a pressureof from about 25 p.'s.i.g. to about p.s.i.g., fractionating the resultant products to separatekthe cul-nene from the phenol, commingling the lastmentioned phenol with'said phenol fraction, and recovering the resultant mixture.

6. In-a process for the recovery of phenol from a reactionmixture resulting from the decomposition of cufrorntlie-resulting reaction mixture a phenol fraction and.; ag phenol-containing aryl `tertiary' alk'ene fraction, i sub- Y f. ject-ing the lastmamed fraction to selective hydrogenation i Atoconvert the aryl tertiary alkene toan aryl tertiary'alkane vmene hydroperoxide and comprising said phenol,l acetone,

alpha, alpha-dimethylbenzyl alcohol, alpha-methyl styrene,

and cumene, the improvement'Which comprises passing said reaction mixture to al separation Vzone 4and therein distilling the acetone fraction from said reactitm-mixture,y

passing the acetone-free reactionv mixture to a dehydration zone and thereinfdehydrating vthe alphen.,alpha-dimethyl- C. and at a reduced pressure off frorn'about v3.2 Hg to aboutI 9.4 Hg, separating the resjultin'glreaction mixture into a phenol-fraction, an` alpharnethyl styrene-phenol y' Y `fraction, and a cumene fractionatfsubstantiallythe afore-l 15 said conditions of reduced pressure,separately/'recovering the cumene fraction and the phenol -fraction, conducting Ythe alpha-methyl styrene-phenol fraction to a hydrogenation zone and converting the alpha-methyl styrene vto Cumcne therein by -contacting .said alpha-methyl styrene-v 20 -phenol fractionwith hydrogen in the presence ofa hydrogenation catalyst comprising a metal of Group'VIII at a temperature offrom about 20 C. to about 75 C.

and at a pressure of vfrom about 325 p.s.i.g. vto about v125 p.s.i.g., passing the resulting cumene-phenol solution to a I fractionation zone and therein separating the cumene as the overhead distillate from the phenol, and c'ommingling the latter with said phenol faction for recoverytherewith.

ReferencesCited in the le of this patent UNITED STATES PATENTS 2,715,145 2,728,793 12/55 Armstrong et al. ---42260-621 2,824,049 2/58 Maincon et al a- 2601-7621 p n FOREIGN PATENTS 802,054 '9p/58 Great Britain.

OTHER REFERENCES 5 Voronkov et 111.," Chem. Abstracts, 44:19`55 -1,956 (1950) (1 page). v l g LEONAZITVER, Primary Examiner. Y CHARLES B. PARKER, G. MOORE, l

' Examiners. 

1. IN A PROCESS FOR THE RECOVERY OF A PHENOL FROM A REACTION MIXTURE RESULTING FROM THE DECOMPOSITION OF AN ARALKYL TERTIARY HYDROPEROXIDE AND COMPRISING SAID PHENOL, A KETONE, AN ARYL TERTIARY ALKANOL AND AN ARYL TERTIARY ALKENE, THE IMPROVEMENT WHICH COMPRISES DISTILLING THE KETONE FROM SAID REACTON MIXTURE, SUBJECTING THE KETONFREE MIXTURE TO DEHYDRATION TO COVERT THE ARYL TERTIARY ALKANOL INTO ADDITIONAL ARYL TERTIARY ALKENE, SEPARATING FROM THE RESULTING REACTION MIXTURE A PHENOL FRACTION AND A PHENOL-CONTAINING ARYL TERIARY ALKENE FRACTION, SUBJECTING THE LAST-NAMED FRACTION TO SELECTIVE HYDROGENATION TO CONVERT THE ARYL TERTIARY ALKENE TO AN ARYL TERTIARY ALKANE WITHOUT HYDROGENATION OF THE PHENOL BY CONTACTING SAID LAST-NAMED FRACTION WITH HYDROGEN IN THE PRESENCE OF A HYDROGENATION CATALYST COMPRISING A GROUP VIII METAL AT A TEMPERATURE OFF ROM ABOUT 20*C. TO ABOUT 75*C. AND AT A PRESSURE OF FROM ABOUT 25 P.S.I.G. TO ABOUT 125 P.S.I.G., FRACTIONATING THE RESULTANT PRODUCTS TO SEPARATE SAID ALKANE FROM THE PHENOL, COMMINGLING THE LAST-MENTIONED PHENOL WITH SAID PHENOL FRACTION AND RECOVERING THE RESULTANT MIXTURE. 